Classifications

• • C—CHEMISTRY; METALLURGY
  • C07—ORGANIC CHEMISTRY
  • C07D—HETEROCYCLIC COMPOUNDS
  • C07D211/00—Heterocyclic compounds containing hydrogenated pyridine rings, not condensed with other rings
  • C07D211/04—Heterocyclic compounds containing hydrogenated pyridine rings, not condensed with other rings with only hydrogen or carbon atoms directly attached to the ring nitrogen atom
  • C07D211/80—Heterocyclic compounds containing hydrogenated pyridine rings, not condensed with other rings with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having two double bonds between ring members or between ring members and non-ring members
  • C07D211/84—Heterocyclic compounds containing hydrogenated pyridine rings, not condensed with other rings with only hydrogen or carbon atoms directly attached to the ring nitrogen atom having two double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms, with at the most one bond to halogen directly attached to ring carbon atoms
  • C07D211/90—Carbon atoms having three bonds to hetero atoms with at the most one bond to halogen

Definitions

• the invention relates generally to the preparation of dihydropyridines and derivatives thereof, and more particularly to the preparation of felodipine.
• Felodipine, Formula 1 is a 1,4 dihydropyridine derivative for use as an antihypertensive and muscle relaxant drug.
• Other phenyl-1,4 dihydropyridine compounds have been disclosed which have therapeutic activity in the treatment of heart disease, see U.S. Pat. No. 5,310,917. ##STR1##
• the preparation of felodipine and related compounds typically involves a multistep synthesis, the last step of which usually involves formation of the dihydropyridine ring.
• U.S. Pat. No. 5,310,917 describes a synthesis involving heating a mixture of a benzylidine with an amino crotonate ester in the presence of a strong acid to yield the desired dihydropyridine product
• U.S. Pat. No. 4,600,778 describes a process for the preparation of dihydropyridine compounds by reacting a ketocarboxylic ester with an aldehyde, and a catalytic amount of piperidine acetate in an aliphatic alcohol as solvent. Both patents are herein incorporated by reference in their entirety.
• Disadvantages with most of the disclosed syntheses for the preparation of dihydropyridine derivatives, and in particular felodipine include (1) an extractive workup to isolate the desired product; (2) the formation of symmetrical ester byproducts which are difficult to isolate from the desired final compound; (3) use of acids in the reaction which require a neutralization step(s) to remove.
• the extractive workup and removal of byproducts are labor intensive procedures. From a commercial viewpoint, the use of acids is often costly and environmentally unfriendly. It is preferred to avoid their use and any potential dangers associated with the use of acids.
• aryl refers to aromatic moieties, for example phenyl.
• Substituents refers to one or more substituent selected from nitro, halo, C 1-6 alkyl, C 1-6 alkoxy, hydroxy, trifluoromethyl, and cyano; alkyl and alkoxy chains may be linear or branched; halo or halogen refers to chloro, fluoro, bromo, and iodo.
• Aryl substitutents may be placed anywhere in the ring.
• the present invention relates broadly to the preparation of dihydropyridine compounds and derivatives thereof, and more particularly felodipine.
• the invention is described in particular detail with respect to the preparation of felodipine.
• dihydropyridine compounds such as nitedipine, amlodipine, isradipine, and the like, it is understood by those of skill in the art that a similar procedure may be employed.
• the respective starting aldehyde and ketone compounds are employed.
• the process to prepare felodipine involves a two step procedure. First, condensing 2,3-dichlorobenzaldehyde with alkyl, (eg. methyl or ethyl), acetoacetate in the presence of a catalyst system. Second, contacting the resultant benzylidine intermediate with alkyl (eg. methyl or ethyl), aminocrotonate to provide felodipine in high yields.
• alkyl eg. methyl or ethyl
• aminocrotonate e.g. methyl or ethyl
• the novelty of the present invention resides in part on (1) a new catalyst system not previously disclosed for the preparation of the felodipine intermediate, (2) the absence of an acid(s), (3) the control of reaction conditions to yield lower amounts of unreacted aldehyde compared to literature reaction conditions, (4) a simplified purification process, and (5) formation of negligible quantities of symmetrical diester byproducts.
• This reduction in unreacted aldehyde content is especially important since it affects the outcome of the symmetrical diester impurity formation in the production of felodipine product.
• the new catalyst system for the preparation of dihydropyridine compounds comprises a mixture of (I) a carboxylic acid compound having the formula, ##STR2## wherein R 1 , R 2 , and R 3 are independently H, halogen, C 1-6 alkyl, aryl, substituted aryl, NO 2 ; Z is independently H, halogen, NO 2 , OCH 3 , OH and, (II) a secondary amine such as N-methyl benzylamine, dimethylamine, diethylamine, diisopropylamine, diisopropylalkylamine wherein alkyl is C 1-6 , and the like, to form a benzylidine intermediate ("MBI").
• MBI benzylidine intermediate
• the resulting benyzlidine intermediate is then reacted with alkyl or alkylaryl aminocrotonate, e.g., ethylaminocrotonate, methylaminocrotonate, in the absence of an acid to yield the desired product.
• alkyl or alkylaryl aminocrotonate e.g., ethylaminocrotonate, methylaminocrotonate
• an alcoholic solvent preferably having between 1 and 6 carbon atoms is employed in the reactions.
• a short chain (e.g. C 5-10 ) aliphatic hydrocarbon may be employed as solvent.
• Suitable reaction conditions for the inventive process include a general temperature range for the first step of the reaction of between about 45° C. to about 65° C. and a reaction time of between about 3 to about 18 hours. A catalytic amount of the catalyst system is employed. Alternatively, the MBI may be treated in-situ with the aminocrotonate derivative to furnish the desired product.
• Suitable reaction conditions for the second reaction include a temperature range of about reflux of the solvent, for a reaction time of preferably less than about 1 hour.
• the present invention relates broadly to a process for the preparation of dihydropyridine compounds and particularly to the preparation of felodipine.
• the synthesis may be applied to the preparation of similar antihypertensive drugs such as amlodipine, cronidipine, diperdipine, furaldipine, isradipine, lacidipine, manidipine, mepirodipine, nifedipine, nivaldipine, nimodipine, nisoldipine, nitendipine, sagandipine and taludipine and the like.
• the following synthetic scheme illustrates a reaction sequence for the production of felodipine. ##STR3## R and R' are C 1-6 alkyl, preferably C 1-2 .
• MAA is methyl acetoacetate
• DCB is 2,3-dichlorobenzaldehyde
• R is C 1
• MBI is methyl benzylidine intermediate.
• EAC is Ethyl 3-aminocrotonate.
• the present invention relates broadly to a process for the preparation of a dihydropyridine compound comprising contacting under suitable reaction conditions
• R 1 , R 2 , and R 3 are independently H, halogen, C 1-6 alkyl, C 1-6 alkoxy, alkylaryl, aryl and substituted aryl wherein substitutents may be in any position;
• Z is independently H, halogen, NO 2 , OCH 3 , OH, and,
• a substituted or unsubstituted secondary amine such as a dialkyl amine, such as diethylamine dimethylamine, diisopropylamine, N-methyl benzylamine, and the like, to form a benzylidine intermediate; and,
• the present invention relates to the preparation of felodipine comprising contacting under suitable reaction conditions (a) 2,3-dichlorobenzaldehyde, methyl acetoacetate, and a catalytic amount of an carboxylate salt of an amine which salt may comprise a mixture of (I) and (II) as identified above to form a benzylidine intermediate; and, (b) contacting said benzylidine intermediate with EAC in the absence of an acid.
• One embodiment of the present invention involves, as step (a), the synthesis of methyl benzylidine as an intermediate (MBI).
• BBI 2,3-dichlorobenzaldehyde is condensed with methyl acetoacetate in the presence of a catalytic amount of an carboxylate salt of an amine.
• the reaction is conducted in an alcoholic solvent at a temperature in the range of about 45° C. to about 65° C., at atmospheric pressures, and for a time of about 3 to about 18 hours.
• step(a) employs aromatic aldehyde compounds having the general formula 2 ##STR7## wherein X 1 and X 2 are as previously defined.
• Exemplary aromatic benzaldehydes include but are not limited to, 2- or 3-nitrobenzaldehyde, 2,3-diichlorobenzaldehyde, 2,1,3-benzoxadiazole-4-aldehyde, and the like.
• ketocarboxylic acids include but are not limited to ethyl acetoacetate, methyl acetoacetate, cyclopropyl acetoacetate, isopropylacetoacetate, and the like.
• aldehyde and carboxylic acid are reacted in a molar ratio of about 0.5-2.0, preferably about 0.8-1.0 and most preferably about 0.9.
• Exemplary catalyst systems include but are not limited to carboxylate or benzoate salts of amines such as the salt mixture of N-methyl benzylamine, diethylamine, dimethylamine, isopropylethylamine, isopropylmethylamine, and the like, and chloroacetic acid, phenylacetic acid, benzoic acid, and the like.
• Catalyst is employed in a sufficient amount to catalyze the reaction.
• the catalyst is generally added in amounts of about 0.04 to about 0.20 equivalents of aldehyde, preferably about 0.6-0.10, and most preferably about 0.06-0.08 molar ratio.
• the catalyst component (I) may contain any halogen.
• Chlorine is a preferred halogen substitutent primarily due to commercial availability and cost. It is important to employ a carboxylic acid as a catalyst component.
• Other useful catalyst components include, but are limited to, dihalogen compounds, e.g. dichloroacetic acid, phenylacetic acid, benzoic acid, and the like.
• MBI exists as two isomers (E and Z) and the reaction of 2,3-dichlorobenzaldehyde and methyl acetoacetate generally reaches an equilibrium after about 4 hours.
• This mixture of isomers consists of about 45:55 ratio of E to Z isomer and we have found that predominately one of the two isomers precipitates from solution. The more soluble isomer remains in solution in the filtrate.
• the filtrate is thermally isomerized to regenerate the thermodynamic mixture of isomers that allows us to isolate a second crop and increase our yield.
• step (a) The condensation of step (a) is preferably carried out in a solvent that facilitates the reaction. It has also been found that satisfactory selectivity and yield can be obtained by carrying out the process of step (a) in alcoholic solvents. Generally, an initial concentration of aldehyde of about 10 to about 20 percent (%) by weight (wt) in the solvent is employed.
• Suitable reaction solvents for step (a) include alcohols having between about 1 and 6 carbon atoms and short chain (e.g. C 5-10 ) aliphatic hydrocarbons. Exemplary alcohols include methanol, ethanol, isopropanol, with a preference for isopropanol. Exemplary aliphatic or cycloaliphatic solvents include hexane and cyclohexane. Additional optional solvents which are less preferred include organic aromatics such as benzene, toluene, and the like, and halogenated solvents such as dichloromethane, dichloroethane, chloroform, and the like
• the time of the reaction is only that necessary to complete the reaction and the reaction can generally be carried out at elevated temperature (e.g., refluxing isopropanol) under atmospheric conditions. Generally the reaction proceeds in about 3 to about 18 hours, preferably s about 3 to about 10 hours, and most preferably about 4-6 hours.
• 2,3-dichlorobenzaldehyde is condensed with methyl acetoacetate in isopropanol and heated to an internal temperature of about 60° C.
• the mixture is concentrated by removing distillate at about 45-60° C. and the contents cooled gradually.
• the resultant precipitated MBI is removed by filtration, washed with isopropanol and dried in vacuo (preferably at less than 40° C.).
• the reaction proceeded in about 3-4 hours. If desired, a second crop may be isolated from the recovered filtrate.
• the benzylidine product of step 1 is condensed with a suitably substituted enamine, such as mentioned previously, in a refluxing alcoholic solvent, preferably isopropanol.
• a suitably substituted enamine such as mentioned previously
• a refluxing alcoholic solvent preferably isopropanol.
• the MBI formed during step (A) is preferably isolated and dried and reacted with EAC.
• the MBI is dissolved in isopropanol (preferably in a ratio of approximately 1 ml isopropanol per mmol MBI), and the contents brought to reflux.
• the felodipine reaction is sensitive to the amount of EAC charged during step (B). It has been found that when the EAC charge exceeds about 1 equivalent (per MBI), symmetrical diesters are produced, especially the diethyl ester. These ester impurities are difficult to remove in subsequent purification, therefore, it is strongly recommended to avoid their formation by careful monitor of the initial amount of EAC charged to the reaction.
• the felodipine reaction of step (B) is sensitive to reaction time, particularly in isopropanol solvent.
• the amount of symmetrical diesters increases with time at the expense of the felodipine product.
• the sensitivity of the felodipine reaction to time appears to be less pronounced than the sensitivity of the reaction to the EAC charge.
• U.S. Pat. No. '917 describes the use of strong acid in this step and indicates the acid accelerates the reaction and improves purity of the product. We have found that the acid is not necessary to obtain the final felodipine product in high purity. It is strongly recommended to maintain the reaction at reflux less than 60 minutes. As mentioned, a greater time generally results in formation of symmetrically substituted symmetrical ester byproducts. It has been found that if the reaction is performed for less than 1 hour, symmetrical ester byproducts are generally maintained to about or less than 1% in the reaction. The reaction is generally monitored by liquid chromatography (or some other like means of monitoring known to those skilled in the art) to follow the formation of desired product and byproducts.
• the amount of unreacted aldehyde is usually less than 1:1.5%.
• Sodium bisulfite may be employed to remove any unreacted aldehyde from the reaction of step (A).
• Advantages of the present invention include lack of use of hazardous solvents, and a more efficient, cost effective method to produce felodipine.
• regioisomer ##STR8## (exocyclic double bond) is formed.
• This regioisomer co-precipitates with felodipine and therefore must be converted to felodipine prior to isolation of the desired product.
• this may be accomplished in the absence of an acid by refluxing the crude felodipine in an inert solvent such as cyclohexane.
• an inert solvent such as cyclohexane.
• most solvents having a boiling point of at least about 80° C. are sufficient for this purification step.
• the cyclohexane reflux thermally converts the regioisomer to felodipine. Generally, this conversion will be accomplished in about 6 to about 20 hours.
• Cyclohexane (ca. 2-6 parts) is added to the crude residue of step (B) and a distillation is performed at below 50° C. This procedure is repeated twice, preferably three times with the final residue/cyclohexane addition refluxing at about 80-85° C. at atmospheric pressure for about 6 hours. Provided the thermal conversion of the regioisomer has occurred, the distillation/reflux may be performed for shorter or longer periods of time if desired. It is preferred to monitor the conversion by suitable means to determine complete conversion.
• the resultant felodipine product is in a slurry and may be cooled to about 30-35° C. to obtain felodipine solids which are subsequently isolated and washed with cyclohexane.
• the moist felodipine solids are dissolved in hot methyl tert-butyl ether (MTBE).
• MTBE hot methyl tert-butyl ether
• Alternate solvent systems include ethanol/water mixture, aliphatic, cycloaliphatic such as cyclohexane, or aromatic hydrocarbons. Any solvent or solvent system is acceptable for use at this step provided that the felodipine is at least partially soluble in the hot solvent mixture. Generally the mixture may be hot filtered to clarify the solution. The solution is concentrated, by conventional means, and the MTBE distillates collected. Cyclohexane is added to the resultant residue in an amount to prepare an approximate 80:20 (w/w) MTBE:cyclohexane solvent system and heated.
• the solution is cooled and the recrystallized felodipine is isolated at about 30-35° C.
• the solids are further washed in an 20:80 (w/w) MTBE:cyclohexane mixed solvent system, followed by a cyclohexane wash and dried in vacuo to afford felodipine solids in a purity of greater than 99.5% (area % in accordance with HPLC).
• the present invention has now eliminated acidic solvents, and provides a simplified purification process.
• the combined filtrates and wash were re-heated to about 60 ⁇ 5° C. for 1 hr, and concentrated by removing about 175-225 g of distillate at about 45-65° C. (internal temperature).
• the contents were again gradually cooled in an ice bath to collect a second crop of MBI solids which were isolated by filtration on the same filter funnel containing the first crop solids.
• the combined first and second crop solids were washed with 2 ⁇ 70 g of isopropanol and dried in vacuo ( ⁇ 40° C.).
• a 2 L flask was equipped with a mechanical agitator, nitrogen purge, reflux condenser, addition funnel and internal temperature probe and charged with the MBI solids (about 95 g, 0.35 mol, 1.0 equiv) and 266 ml isopropanol and the contents are brought to reflux.
• a solution of about 0.90 equiv of ethyl 3-aminocrotonate (about 40.4 g EAC for 95 g MBI charge, 0.31 mol, 0.9 equiv) in 96 mL of isopropanol was added to the refluxing solution at such a rate that the internal temperature was maintained at reflux (ca. 83° C. or about 10 min addition time).
• the resulting mixture was kept at reflux for 60-70 min, then the temperature brought down to below 50° C. by (1) removing heat source, (2) adding 96 niL of isopropanol, and (3) vacuum distillation of isopropanol.
• the vacuum distillation was performed at below 50° C. to remove approximately 200-300 g of overhead.
• Cyclohexane (155 g) was added to the residue and the distillation continued at below 50° C. to remove an additional 100-150 g of overhead.
• Another cyclohexane (155 g) portion was added to the residue and the distillation continued at below 50° C. to remove yet another 100-150 g of overhead.
• a third cyclohexane (780 g) portion was added and the contents brought to atmospheric reflux (ca. 80-85° C.) for about 6 hrs.
• the slurry was cooled to about 30-35° C. and the crude felodipine isolated by filtration and washed with 50 g cyclohexane.
• the moist crude felodipine solids were dissolved in about 550 g of methyl tert-butyl ether (MTBE) and hot filtered to clarify the solution.
• the dissolving flask and filter were rinsed with an additional 30 g of MTBE, which was added to the original hot filtrate.
• the MTBE solution was placed in a flask equipped with agitator, nitrogen purge, heat source, temperature probe, distillation head and receiver. The mixture was concentrated by atmospheric distillation to remove MTBE (ca. 550° C. internal temperature). Once 100-250 g of distillate have been collected, cyclohexane was added in an amount to prepare approximately an 80:20 (w/w) MTBE:cyclohexane solvent system.
• the resultant solution was cooled and the recrystallized Felodipine was isolated at about 30-35° C.
• the recrystallized felodipine solids were further washed with 1 ⁇ 70 g of 20:80 (w/w) MTBE:cyclohexane and 1 ⁇ 70 g of cyclohexane.
• the solids were dried in vacuo to afford 45-70 g of pure felodipine solids.
• the residue was dissolved in MBTE and brought to reflux.
• the solution was concentrated and cooled linearly over a period of about 3 hours to ambient temperature.
• the solids which formed were filtered and washed with MBTE/hexane solution to provide felodipine in about 99.4% purity.
• the crude product was dissolved in MBTE under reflux and the solution cooled linearly over about 3 hours to ambient temperature.
• the solids were isolated and further washed with MBTE/hexane solution providing 142 g of felodipine (about 37.7% yield, 99.3% purity, MP 144-45° C.).
• a 3-L flask was equipped with a mechanical agitator, nitrogen purge, reflux condenser, addition funnel, and internal temperature probe was charged with the MBI solids (81.7 g, 0.30 mol), isopropanol (217 mL) and the contents are brought to reflux.
• a solution of ethyl 3-aminocrotonate (31.8 g, 0.25 mol, 0.83 equiv) in isopropanol (102 mL) was added to the refluxing solution at such a rate that the internal temperature was maintained at reflux (ca. 83-85° C. during 10 minute addition). The resulting mixture was kept at reflux for 70 minutes, then the temperature was brought down to below 50° C.
• the moist crude felodipine solids were dissolved in methyl t-butylether (MTBE) (810 mL) and hot filtered to clarify the solution.
• MTBE methyl t-butylether
• the dissolving flask and filter were rinsed with an additional MTBE (40 mL), which was added to the original hot filtrate.
• the MTBE solution was placed in a flask equipped with an agitator, nitrogen purge, heat source, temperature probe, distillation head, and receiver.
• the mixture was concentrated by atmospheric distillation to remove MTBE (internal temperature about 57° C.).
• cyclohexane was added in an amount to prepare approximately an 80:20 (w/w) MTBE:cyclohexane solvent system.
• Felodipine was isolated at about 30-35° C.
• the recrystallized felodipine solids were further washed with a MTBE/cyclohexane mixture (10 g MTBE+40 g cyclohexane) and cyclohexane (90 mL).
• the solids were dried in vacuo to afford pure Felodipine as a light yellow crystalline solid (56.9 g, 59.4% yield based on ethyl 3-aminocrotonate).

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• 1995
  • 1995-12-28 US US08/579,758 patent/US5977369A/en not_active Expired - Fee Related
• 1996
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